JP3738141B2 - Variable oxygen enrichment burner - Google Patents
Variable oxygen enrichment burner Download PDFInfo
- Publication number
- JP3738141B2 JP3738141B2 JP31856998A JP31856998A JP3738141B2 JP 3738141 B2 JP3738141 B2 JP 3738141B2 JP 31856998 A JP31856998 A JP 31856998A JP 31856998 A JP31856998 A JP 31856998A JP 3738141 B2 JP3738141 B2 JP 3738141B2
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- Japan
- Prior art keywords
- oxygen
- inner cylinder
- air
- tip
- combustion
- Prior art date
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- Expired - Fee Related
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Description
【0001】
【発明の属する分野】
本発明は、燃焼バーナに関し、特に酸素を富化した状態で燃焼させる酸素富化率可変バーナに関する。
【0002】
【従来の技術】
従来から、火炎温度や火炎長さを調整するものとして、酸素の分圧比率を変化させた酸素富化空気を使用した酸素空気混合バーナが提供されている。従来の酸素空気混合バーナとしては、空気に酸素を混合した支燃性ガスと燃料ガスとを予混合室に導入し、この予混合室で混合した空燃混合ガスをバーナーノズルから噴出させて炉等の燃焼室内で燃焼させるようにしたもの(図4a参照)や、バーナノズルを内外二重管構造に形成し、内管から燃料ガスを、外管から酸素と空気を混合した支燃性ガスをそれぞれ炉等の燃焼室内に噴出させ、バーナノズル先端で混合させるとともに燃焼させるようにしたもの(図4b参照)が知られている。
【0003】
【発明が解決しようとする課題】
燃料ガスと支燃性ガスとを予混合室に導入し、空燃混合ガスを噴出させる形式の酸素空気混合バーナでは、予混合室に全ガスを導入するようにしてあることから、その構造上酸素富化率を30%以上に上昇させると過剰酸素の影響で炎が飛ぶことになるから、富化率に限界があるという問題がある。また、予混合室で燃料と支燃性ガスとを混合することから、逆火が生じるが余地が残っていた。
【0004】
一方、二重管構造にした酸素空気混合バーナでは、酸素と空気が混合しにくく、火炎が不安定になるという問題があるうえ、富化率を変更しようとすると、点火酸素量に比べて空気量が圧倒的に大きいことから支燃性ガスのトータル流量の変化が大きく、支燃性ガス流速が不安定になるという問題がある。また、燃焼用空気と酸素を予混合させる状態となるため、燃焼用空気中の油分と酸素とが接触して混合室内で燃焼し始めるという問題があった。
【0005】
本発明はこのような点に着目してなされたもので、酸素の富化率を広範囲で自由に選択することができ、かつ安定した火炎を得ることのできる酸素富化率可変バーナを提供することを目的とする。
【0006】
【課題を解決するための手段】
上述の目的を達成するために本発明は、同心配置した直管状の内外筒体と、内外筒体間の空間に内筒体を取り囲む状態で配置した複数の管体とからなり、内筒体内を燃料ガス通路に形成し、内外筒体間の空間を空気供給路に構成し、内筒体を取り囲む状態で配置した複数の管体の内部を酸素供給路に形成し、内筒体の先端部を外筒体の先端部よりも内側に位置させるとともに、酸素供給路を形成している各管体の先端部を内筒体の先端部よりも内側に位置させたことを特徴としている。
【0007】
【発明の作用】
本発明では、同心配置した直管状の内外筒体と、内外筒体間の空間に内筒体を取り囲む状態で配置した複数の管体とでバーナを構成し、内筒体内を燃料ガス通路に形成し、内外筒体間の空間を空気供給路に構成し、内筒体を取り囲む状態で配置した複数の管体の内部を酸素供給路に形成し、内筒体の先端部を外筒体の先端部よりも内側に位置させるとともに、酸素供給路を形成している各管体の先端部を内筒体の先端部よりも内側に位置させていることから、空気中に酸素を噴出して十分混合させ、この混合支燃性ガス中にプロパンガス等の燃料ガスを噴出することになり、空気、酸素、燃料を個別に流量制御することができることになるから、支燃性ガス中の酸素富化率を自由に設定することができることになる。これにより、火炎温度を自由に設定することができるうえ、安定した長さの火炎を得ることができることになる。
【0008】
【発明の実施の形態】
図面は本発明の実施態様を示し、図1は中央縦断面図である。
この酸素富化燃焼バーナは、プロパンガス等の液化石油ガス燃料を送給する燃料ガス供給路となる内筒体(1)と、この内筒体(1)の外周に内筒体(1)と同心状に配置した外筒体(2)と、この外筒体(2)の内周面と内筒体(1)の外周面との間の空間(3)に内筒体(1)の軸芯を中心とする同心円上に内筒体(1)を取り囲む状態で配置した複数の管体(4)と、内外筒体(1)(2)及び各管体(4)を保持している本体部分(5)とで構成してある。
【0009】
本体部分(5)は、燃料ガスを供給する燃料ポート(6)を形成した燃料導入ブロック(7)と、酸素ガスを供給する酸素ポート(8)を形成した酸素導入ブロック(9)と、燃焼用空気を供給する空気ポート(10)を形成したエア導入ブロック(11)とで構成してある。燃料供給路となる内筒体(1)はエア導入ブロック(11)及び酸素導入ブロック(9)を貫通する状態に配置されて両ブロック(11)(9)に支持され、ブロック(7)に固定されている。酸素ガス通路となる各管体(4)はエア導入ブロック(11)を貫通する状態に配置され、エア導入ブロック(11)に出退移動可能な状態で支持されている。また、外筒体(2)はエア導入ブロック(11)の先端面部分に固定されており、外筒体(2)の内部で内筒体(1)との間に形成した空間(3)の基端部は空気ポート(10)に臨んで開口している。したがって、外筒体(2)と内筒体(1)との間に形成される空間(3)が燃焼用空気の供給路となる。なお、この外筒体(2)は二重管で構成してあり、この二重管の内部を冷却水通路(12)に形成してある。
【0010】
内筒体(1)の先端部は外筒体(2)の内部に位置しており、酸素供給路となる各管体(4)の先端部は内筒体(1)の先端部よりもさらに内側に位置させてある。そして、各管体(4)の先端部はノズル(13)に形成してある。なお、酸素供給路となる各管体(4)はその中間部分を内筒体(1)の外周面に固定したホルダー(図示略)で支持してあり、このホルダーは内外筒体(1)(2)間に形成した燃焼用空気供給路(3)を閉塞しない形状に形成してある。
【0011】
図中符号(14)は燃料導入ブロック(7)に接続した燃料供給管、(15)は酸素導入ブロック(9)に接続した酸素供給管、(16)はエア導入ブロック(11)に接続した燃焼用空気供給管であり、各供給管(14)(15)(16)にはそれぞれ流量調整機構が設けてある。
【0012】
燃料としてプロパンガスを使用した場合、燃焼用空気中の酸素濃度と火炎温度は図2に示す関係にあり、一方の燃焼用空気中の酸素濃度と火炎長さは図3に示す関係にある。なお、火炎長さは燃焼用空気中の酸素濃度が21%(大気混合割合)の時の火炎長を100%とした際の割合で示してある。
【0013】
上述の構成からなる酸素富化率可変バーナでは、バーナ部分が炉内に臨む状態で炉体等に本体部分(5)を固定し、所望の燃焼温度と所望の火炎長さから、酸素富化率を設定し、その富化率となる量の酸素を酸素供給管(15)から供給するとともに、燃料供給管(14)からプロパン等の液化石油ガス燃料を、また燃焼用空気供給管(16)から酸素富化率の増減に対応して、供給量が調整された後の燃焼用空気をそれぞれ供給する。
【0014】
各供給管(14)(15)(16)から供給された酸素ガス、燃料ガス、燃焼用空気は途中混ざり合うことなくバーナ先端部まで案内され、着火直前まで個別に供給されることから、逆火が発生することがなくなる。
【0015】
【発明の効果】
本発明では、同心配置した直管状の内外筒体と、内外筒体間の空間に内筒体を取り囲む状態で配置した複数の管体とでバーナを構成し、内筒体内を燃料ガス通路に形成し、内外筒体間の空間を空気供給路に構成し、内筒体を取り囲む状態で配置した複数の管体の内部を酸素供給路に形成し、内筒体の先端部を外筒体の先端部よりも内側に位置させるとともに、酸素供給路を形成している各管体の先端部を内筒体の先端部よりも内側に位置させていることから、空気中に酸素を噴出して十分混合させ、この混合支燃性ガス中にプロパンガス等の燃料ガスを噴出することになり、空気、酸素、燃料を個別に流量制御することができることになるから、支燃性ガス中の酸素富化率を自由に設定することができることになる。これにより、火炎温度を自由に設定することができるうえ、安定した長さの火炎を得ることができる。
【0016】
また、燃料ガスや燃焼用空気、富化用酸素ガスは、バーナ内で別個に供給され、混合直後に点火して燃焼することになるから、ガスの雰囲気が燃焼可能範囲になる時間及び範囲が極めて短く、逆火が発生することはない。
【図面の簡単な説明】
【図1】中央縦断面図である。
【図2】酸素富化率と燃焼温度の関係を示す図である。
【図3】酸素富化率と火炎長の関係を示す図である。
【図4】従来の酸素空気混合バーナを概略的に示す図であり、図4(a)は予混合室構造の酸素空気混合バーナ、図4(b)は二重管構造の酸素空気混合バーナの概略斜視図である。
【符号の説明】
1…内筒体、2…外筒体、4…管体、3…内外筒体間の空間。[0001]
[Field of the Invention]
The present invention relates to a combustion burner, and more particularly to a variable oxygen enrichment burner that burns in a state enriched with oxygen.
[0002]
[Prior art]
Conventionally, oxygen-air mixing burners using oxygen-enriched air in which the partial pressure ratio of oxygen is changed have been provided to adjust the flame temperature and flame length. As a conventional oxygen-air mixed burner, a combustion-supporting gas in which oxygen is mixed with air and a fuel gas are introduced into a premixing chamber, and an air-fuel mixture gas mixed in the premixing chamber is ejected from a burner nozzle to a furnace. A combustion chamber such as a combustion chamber (see FIG. 4a), or a burner nozzle formed in an inner / outer double tube structure, fuel gas from the inner tube, and combustion-supporting gas in which oxygen and air are mixed from the outer tube. There are known those which are jetted into a combustion chamber such as a furnace, mixed at the tip of a burner nozzle and burned (see FIG. 4b).
[0003]
[Problems to be solved by the invention]
In an oxygen-air mixing burner in which fuel gas and combustion-supporting gas are introduced into the premixing chamber and the air-fuel mixture gas is ejected, the entire gas is introduced into the premixing chamber. If the oxygen enrichment rate is increased to 30% or more, the flame will fly under the influence of excess oxygen, so there is a problem that the enrichment rate is limited. Further, since the fuel and the combustion-supporting gas are mixed in the premixing chamber, a backfire occurs, but there is room for it.
[0004]
On the other hand, oxygen-air mixing burners with a double-pipe structure have a problem that oxygen and air are difficult to mix and the flame becomes unstable, and when trying to change the enrichment rate, the air is compared to the amount of ignition oxygen. Since the amount is overwhelmingly large, there is a problem that the change in the total flow rate of the combustion-supporting gas is large and the flow rate of the combustion-supporting gas becomes unstable. Further, since the combustion air and oxygen are premixed, there is a problem that the oil in the combustion air and oxygen come into contact with each other and start to burn in the mixing chamber.
[0005]
The present invention has been made paying attention to such points, and provides an oxygen enrichment variable burner capable of freely selecting an oxygen enrichment over a wide range and obtaining a stable flame. For the purpose.
[0006]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, the present invention comprises a straight tubular inner and outer cylindrical bodies arranged concentrically, and a plurality of tubular bodies arranged in a state surrounding the inner cylindrical body in a space between the inner and outer cylindrical bodies. Formed in the fuel gas passage, the space between the inner and outer cylinders is configured as an air supply path, the inside of a plurality of tubes arranged in a state surrounding the inner cylinder is formed in the oxygen supply path, and the tip of the inner cylinder The tube is positioned inside the tip of the outer cylinder, and the tip of each tube forming the oxygen supply path is positioned inside the tip of the inner cylinder.
[0007]
[Effects of the Invention]
In the present invention, a burner is constituted by a straight tubular inner and outer cylinders arranged concentrically and a plurality of pipes arranged in a state surrounding the inner cylinder in a space between the inner and outer cylinders, and the inner cylinder is used as a fuel gas passage. Forming a space between the inner and outer cylinders in the air supply path, forming the interior of a plurality of tubes arranged in a state surrounding the inner cylinder in the oxygen supply path, and forming the tip of the inner cylinder as the outer cylinder Since the tip of each tube forming the oxygen supply path is located inside the tip of the inner cylinder, the oxygen is blown out into the air. The fuel gas such as propane gas is injected into this mixed combustion-supporting gas, and the flow rate of air, oxygen, and fuel can be individually controlled. The oxygen enrichment rate can be set freely. Thereby, the flame temperature can be set freely, and a flame having a stable length can be obtained.
[0008]
DETAILED DESCRIPTION OF THE INVENTION
The drawings show an embodiment of the present invention, and FIG. 1 is a central longitudinal sectional view.
The oxygen-enriched combustion burner includes an inner cylinder (1) that serves as a fuel gas supply passage for supplying liquefied petroleum gas fuel such as propane gas, and an inner cylinder (1) on the outer periphery of the inner cylinder (1) The outer cylinder (2) arranged concentrically with the inner cylinder (1) in the space (3) between the inner peripheral surface of the outer cylinder (2) and the outer peripheral surface of the inner cylinder (1) A plurality of tubes (4) arranged in a state of surrounding the inner cylinder (1) on a concentric circle centering on the axis of the inner tube, the inner and outer cylinders (1) (2), and each tube (4) are held. And a main body portion (5).
[0009]
The main body portion (5) includes a fuel introduction block (7) in which a fuel port (6) for supplying fuel gas is formed, an oxygen introduction block (9) in which an oxygen port (8) for supplying oxygen gas is formed, and a combustion And an air introduction block (11) having an air port (10) for supplying working air. The inner cylindrical body (1) serving as a fuel supply path is disposed so as to penetrate the air introduction block (11) and the oxygen introduction block (9) and is supported by both blocks (11) and (9). It is fixed. Each tubular body (4) serving as an oxygen gas passage is disposed in a state of penetrating the air introduction block (11), and is supported by the air introduction block (11) in a state in which it can be moved back and forth. The outer cylinder (2) is fixed to the front end surface portion of the air introduction block (11), and a space (3) formed between the outer cylinder (2) and the inner cylinder (1). The base end portion of this is open to face the air port (10). Accordingly, the space (3) formed between the outer cylinder (2) and the inner cylinder (1) serves as a supply path for combustion air. The outer cylinder (2) is a double pipe, and the inside of the double pipe is formed in the cooling water passage (12).
[0010]
The tip of the inner cylinder (1) is located inside the outer cylinder (2), and the tip of each tube (4) serving as an oxygen supply path is more than the tip of the inner cylinder (1). Furthermore, it is located inside. And the front-end | tip part of each pipe body (4) is formed in the nozzle (13). Each tube (4) serving as an oxygen supply path is supported by a holder (not shown) whose intermediate portion is fixed to the outer peripheral surface of the inner cylinder (1). (2) The combustion air supply passage (3) formed between them is formed in a shape that does not close.
[0011]
In the figure, reference numeral (14) is a fuel supply pipe connected to the fuel introduction block (7), (15) is an oxygen supply pipe connected to the oxygen introduction block (9), and (16) is connected to the air introduction block (11). It is a combustion air supply pipe, and each of the supply pipes (14), (15) and (16) is provided with a flow rate adjusting mechanism.
[0012]
When propane gas is used as the fuel, the oxygen concentration in the combustion air and the flame temperature have the relationship shown in FIG. 2, and the oxygen concentration in one combustion air and the flame length have the relationship shown in FIG. The flame length is shown as a ratio when the flame length is 100% when the oxygen concentration in the combustion air is 21% (atmospheric mixing ratio).
[0013]
In the oxygen enrichment variable burner configured as described above, the main body portion (5) is fixed to the furnace body or the like with the burner portion facing the furnace, and the oxygen enrichment is performed from a desired combustion temperature and a desired flame length. The oxygen is supplied from the oxygen supply pipe (15), the liquefied petroleum gas fuel such as propane from the fuel supply pipe (14), and the combustion air supply pipe (16 ) To supply the combustion air after the supply amount is adjusted in accordance with the increase or decrease of the oxygen enrichment rate.
[0014]
The oxygen gas, fuel gas, and combustion air supplied from each supply pipe (14), (15), and (16) are guided to the burner tip without being mixed in the middle, and are supplied individually until immediately before ignition. There will be no fire.
[0015]
【The invention's effect】
In the present invention, a burner is constituted by a straight tubular inner and outer cylinders arranged concentrically and a plurality of pipes arranged in a state surrounding the inner cylinder in a space between the inner and outer cylinders, and the inner cylinder is used as a fuel gas passage. Forming a space between the inner and outer cylinders in the air supply path, forming the interior of a plurality of tubes arranged in a state surrounding the inner cylinder in the oxygen supply path, and forming the tip of the inner cylinder as the outer cylinder Since the tip of each tube forming the oxygen supply path is located inside the tip of the inner cylinder, the oxygen is blown out into the air. The fuel gas such as propane gas is injected into this mixed combustion-supporting gas, and the flow rate of air, oxygen, and fuel can be individually controlled. The oxygen enrichment rate can be set freely. Thereby, the flame temperature can be set freely, and a flame having a stable length can be obtained.
[0016]
In addition, fuel gas, combustion air, and enrichment oxygen gas are separately supplied in the burner and ignited and burned immediately after mixing. It is extremely short and does not cause backfire.
[Brief description of the drawings]
FIG. 1 is a central longitudinal sectional view.
FIG. 2 is a graph showing a relationship between an oxygen enrichment rate and a combustion temperature.
FIG. 3 is a graph showing the relationship between the oxygen enrichment rate and the flame length.
4A and 4B are diagrams schematically showing a conventional oxygen-air mixing burner, in which FIG. 4A is an oxygen-air mixing burner having a premixing chamber structure, and FIG. 4B is an oxygen-air mixing burner having a double-pipe structure. FIG.
[Explanation of symbols]
DESCRIPTION OF
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31856998A JP3738141B2 (en) | 1998-11-10 | 1998-11-10 | Variable oxygen enrichment burner |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31856998A JP3738141B2 (en) | 1998-11-10 | 1998-11-10 | Variable oxygen enrichment burner |
Publications (2)
Publication Number | Publication Date |
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JP2000146129A JP2000146129A (en) | 2000-05-26 |
JP3738141B2 true JP3738141B2 (en) | 2006-01-25 |
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JP31856998A Expired - Fee Related JP3738141B2 (en) | 1998-11-10 | 1998-11-10 | Variable oxygen enrichment burner |
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Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
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DE10248530B4 (en) * | 2002-10-14 | 2004-08-12 | Thermoselect Ag | Oxygen lance for high-temperature gasification of waste, and method for operating the same |
US20070231761A1 (en) * | 2006-04-03 | 2007-10-04 | Lee Rosen | Integration of oxy-fuel and air-fuel combustion |
EP1889816A1 (en) * | 2006-08-15 | 2008-02-20 | Rockwool International A/S | Process and apparatus for making mineral fibres |
KR100867743B1 (en) * | 2008-07-04 | 2008-11-10 | 박정재 | The oxygen-burner is had oxygen nozzle improving for the oxygen and fuel mixing |
BRPI0917907A2 (en) * | 2008-08-29 | 2015-11-10 | L Air Liquide Société Anonyme Pour L Etude Et L Expl Des Procedes Georges Claude | method for generating combustion by means of a burner assembly and burner assembly for the same |
JP7091377B2 (en) * | 2020-01-31 | 2022-06-27 | 大陽日酸株式会社 | Oxygen enriched burner and its combustion method |
CN112856454A (en) * | 2021-01-18 | 2021-05-28 | 煤科院节能技术有限公司 | Exhaust gas treatment device and exhaust gas treatment method |
-
1998
- 1998-11-10 JP JP31856998A patent/JP3738141B2/en not_active Expired - Fee Related
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